Pressurized steam boilers and their control

ABSTRACT

A method of controlling the operation of a pressurised steam boiler ( 50 ) heated by a burner ( 20 ), which includes the steps of a) monitoring the level of water in the boiler ( 50 ), b) monitoring the pressure of steam in the boiler ( 50 ), c) monitoring the firing rate of the burner ( 20 ), and d) controlling the flow rate of water into the boiler ( 50 ) having regard to the signals resulting from a) and b) and, at least for some signal conditions, also having regard to signals resulting from c). The level of water is detected by a pair of capacitance probe assemblies ( 58 A and  58 B).

CROSS-REFERENCE TO RELATED APPLICATIONS

Not Applicable

STATEMENT REGARDING FEDERALLY SPONSORED RESEARCH OR DEVELOPMENT

Not Applicable

INCORPORATION-BY-REFERENCE OF MATERIAL SUBMITTED ON A COMPACT DISC

Not Applicable

FIELD OF THE INVENTION

The invention relates to pressurised steam boilers and their control, to a method and apparatus for detecting the level of water in a steam boiler and to a method and apparatus for assessing the mass flow of steam from a steam boiler.

BACKGROUND OF THE INVENTION

In a known arrangement of a pressurised steam boiler, water is fed into the boiler at a controlled rate and is heated in the boiler to convert the water to steam. The heat required to convert the water to steam is provided by a burner whose hot products of combustion are passed through ducts in the boiler and then exhausted. The steam boiler is controlled by a boiler control system, which receives information from sensors indicating inter alia the level of water in the boiler and the presence of steam in the boiler, and which controls the flow rate of water into the boiler as well as sending a control signal to a burner control system that controls the burner. The burner control system controls inter alia the flow of fuel and gas to the burner head in dependence upon a demand signal received from the boiler.

Pressurised steam boilers are potentially very hazardous because of the very high pressure that is maintained in the boiler and it is therefore essential for such boilers to have control systems that are extremely safe. One factor that is taken into account to ensure the safety of a system is the importance of maintaining the water level in the boiler within predetermined limits. The internationally recognised safety regime concerning adequate water level in pressurised steam boilers requires sensing arrangements to detect a first low water level (“first low”) below the normal operating range of the boiler and also to detect a second low water level that is even lower than the first low water level. When the first low water level is detected, the boiler control system sends a signal to the burner control system causing the burner to be switched off. Provided the water level then rises back above the first low water level the boiler control system sends a further signal to the burner control system allowing the burner to restart. If, however, the water level continues to fall and reaches the second low water level, the boiler control system sends a further signal to the burner control system preventing it from restarting without manual intervention. The requirement for manual intervention is inconvenient, but is regarded as a necessary safety requirement.

The false triggering of either the first low or second low is costly. The effect of a false triggering at the first low is to turn off the burner; at best that may simply lead to less efficiency because the burner is switched completely off rather than simply being turned down to a lower firing rate; in a worst case, however, as will be explained below, the false triggering may lead to the burner being switched off at a time when the demand for heat in the boiler is especially high. False triggering at the second low is more damaging because it is likely to last longer given that the burner can be restarted only after manual intervention.

False triggering can occur without any fault in the equipment. In particular, it is not unusual for there to be a sudden demand for steam from a steam boiler; in that case there may be a significant drop in pressure within the boiler which can cause the water level in the boiler to rise (because of the small bubbles of compressed gas trapped within the water in the boiler). The reduction in pressure rightly leads to a signal passing from the boiler control system to the burner control system to increase the firing rate of the burner, while the increase in water level in the boiler causes the usual water flow into the boiler to be reduced or stopped. As the system then recovers and the pressure in the boiler rises, the water level in the boiler falls quickly and may well fall below the “first low” leading to the burner being turned off at a time when it should be operating, probably at full capacity. It is even possible that the fall in water level will reach the “second low” so that the burner remains off until an operator resets the system.

Safety considerations also have an impact on the techniques that are employed to measure the level of water in the boiler. Because of the importance of detecting the “first low” and the “second low”, separate probes are used to detect each of the levels; whilst one capacitative probe may sometimes be provided to sense water levels within the normal operating range, respective conductive probes, which sense whether or not they are in the water, but give no further indication of water level, are provided to detect the “first low” and the “second low”. Often other conductive probes are set at other levels so that those other levels can be detected in a similar way. Thus a large number of separate probes are provided. A capacitative probe is not regarded as sufficiently reliable for detecting the “first low” and the “second low” water levels. Particular concerns are that the signals from such probes are affected by temperature variations and may also be affected by stray electromagnetic radiation generated by devices in the vicinity of the probes.

A further problem when attempting to measure water levels in steam boilers is that whenever the water is boiling a certain amount of turbulence is present, making it difficult to measure the water level accurately.

Operators of pressurised steam boilers frequently purchase steam flow meters to measure the steam flows in the steam exit lines from each of the boilers. A frequent reason for installing such meters is for auditing purposes, to enable the amount of steam exported from the boiler to be compared to the amount of fuel used by the boiler. Such meters are, however, expensive.

BRIEF SUMMARY OF THE INVENTION

It is an object of the invention to provide an improved method and apparatus for controlling the operation of a steam boiler.

It is a further object of the invention to provide a method and apparatus for controlling the operation of a steam boiler in which the likelihood of a burner being shut down unnecessarily is reduced.

It is a further object of the invention to provide an improved method and apparatus for detecting the level of water in a pressurised steam boiler, and especially to provide a method and apparatus in which the number of probes that are required is reduced.

It is a still further object of the invention to provide a method and apparatus for assessing the mass flow of steam from a pressurised steam boiler without resorting to a steam flow meter.

It is a still further object of the invention to provide a method and apparatus for monitoring turbulence in a pressurised steam boiler.

According to the invention there is provided a method of controlling the operation of a steam boiler heated by a burner, the method including the following steps:

-   -   a) monitoring the level of water in the boiler,     -   b) monitoring the pressure of steam in the boiler,     -   c) monitoring the firing rate of the burner, and     -   d) controlling the flow rate of water into the boiler having         regard to the signals resulting from a) and b) and, at least for         some signal conditions, also having regard to signals resulting         from c).

By using the firing rate of the burner as one of the control inputs for determining the flow rate of water into the boiler and in that respect combining the burner control system and the boiler control system, it becomes possible to effect a more appropriate control of the water, reduce the number of times that the water level in the boiler falls below a first low water level at which the burner is switched off and thereby improve the efficiency of the boiler.

Whilst it is within the scope of the invention for the control of the flow rate of water into the boiler always to take account of signals resulting from monitoring the firing rate of the burner, it may be that the signals resulting from monitoring the firing rate of the burner are taken into account in a limited set of circumstances only. It is for example preferred that when

-   -   i) the monitoring of the level of water in the boiler shows a         rate of increase above a predetermined level,     -   ii) the monitoring of the pressure of steam in the boiler shows         a reduction in pressure at a rate above a predetermined level,         and     -   iii) the monitoring of the firing rate of the burner shows that         the firing rate is increasing at a rate above a predetermined         level,     -   the controlling of the flow rate of water into the boiler is         such that it does not necessarily reduce the rate of flow into         the boiler.

Preferably, said controlling of the flow rate of water into the boiler is such that it does not reduce the rate of flow into the boiler, unless the level of water in the boiler is above an upper normal working limit. In a case where there is a sudden demand for steam so that the steam pressure drops quickly and the water level in the boiler increases rapidly, the flow rate of water into the boiler is controlled in dependence upon what is concurrently happening to the firing rate of the burner: if the firing rate of the burner is increasing at a rate above a predetermined level, then that is an indication that the drop in steam pressure is a result of increased demand and that the increase in boiler water level is misleading, and the rate of flow of water into the boiler is not reduced. Since water continues to flow into the boiler the likelihood of the water level dropping below the first or second low water levels is significantly reduced.

An example of a situation where the monitoring of the firing rate would still lead to a reduction in the rate of flow of water into the boiler is given below: when

-   -   i) the monitoring of the level of water in the boiler shows an         increase in level but at a rate of increase below a         predetermined level.     -   ii) the monitoring of the pressure in the boiler shows an         increase in pressure but at a rate of increase below a         predetermined level, and     -   iii) the monitoring of the firing rate of the burner shows that         the firing rate is reducing     -   the controlling of the flow rate of water into the boiler is         such that it does reduce the rate of flow into the boiler.

Preferably, input and output signals relating to all the monitoring and controlling steps are passed into or transmitted from a common control unit that also controls the operation of the burner. The integration of the boiler control unit and burner control unit into a single control unit simplifies, improves and makes cheaper the control of the burner and boiler.

Where reference is made above to a rate of increase above a predetermined level, it is within the scope of the invention for the rate of increase to be at any level above zero. It is preferred, however, that the predetermined level corresponds to what is to be regarded as a normal rate of increase during ordinary operation of the burner and boiler. Appropriate predetermined levels may be determined by a commissioning engineer during commissioning of the system and a rate of increase may be obtained by measuring the increase in values over a time period of the order of 20 seconds.

Where reference is made to monitoring a variable, it should be understood that the variable itself may not be directly sensed but rather one or more other variables, from which the variable being monitored can be calculated, may be sensed.

For example, the firing rate of the burner need not be directly sensed and the pressure of the water in the boiler may be sensed to indicate the pressure of the steam.

In an especially preferred method, the step of monitoring the level of water in the boiler includes the steps of providing a pair of capacitance probe assemblies mounted in the boiler with each of the probes extending through a range of water levels, the probes being arranged such that the capacitance of each probe varies according to the level of the water, and of measuring the capacitance of each probe, comparing the capacitances to one another to check that they match and using the measurement of the capacitance as an indication of the water level. By providing a capacitance probe assembly to measure the water level in the boiler it becomes possible to measure a wide range of levels and, if desired, all the intermediate levels without a large number of probes. Furthermore, by providing a pair of probes that measure the same levels, safety can be considerably improved. Of course, more than two probes can be employed, if desired.

The method may further include the step of shutting down the burner in the event that a discrepancy between the capacitances of the probes exceeds a given level.

The range of water levels through which the probes extend preferably includes a first low water level below the normal working range. Thus the probes are preferably used to detect the “first low”. Furthermore, the range of water levels through which the probes extend preferably includes a second low water level below the first low water level. Thus the probes are preferably also used to detect the “second low”. Conventional capacitative probes have not been regarded as satisfactory for detecting the “first low” and “second low” because of the importance, from a safety point of view, of that detection. We have found, however, that by using a pair of probes to make the same measurements it is possible to provide a very safe detecting arrangement.

It is still further preferred that the range of water levels through which the probes extend include all other water levels that are to be detected. In that case there is no need to provide any other water level detectors apart from the probes. The further water levels detected by the probes may be the limits of the normal working range of water level and/or a high water level above the normal working range and/or other levels which may be required by particular laws or codes of practice in a given country.

Each of the capacitance probes preferably projects downwardly from an upper region of the boiler housing. Each probe preferably comprises an elongate core of electrically conducting material surrounded by a sleeve of electrically insulating material.

Preferably the pair of capacitance probe assemblies are substantially identical.

Each capacitance probe assembly preferably includes in addition a reference capacitance whose capacitance value is sensed alternately with the probe capacitance value. By providing such a reference capacitance value in each probe assembly, it is possible to detect any distortion of the sensed value of capacitance that might arise. A cause of such a discrepancy would be a change in the temperature of the probe assembly. That would change the sensed values of both the reference capacitance and the probe capacitance and, since the reference capacitance is known, enables a correction to be made to the sensed value of the probe capacitance. Furthermore, if desired, a temperature monitoring device can be provided in the probe assembly and can, via for example a look-up table, calculate a correction to be made to the sensed value of the probe capacitance; a check can then be made that the two different methods of correcting the sensed value of the probe capacitance do not differ by more than a given amount and, if they do, the burner can be shut down. Another cause of such a discrepancy might arise, for example, from electromagnetic radiation. We have found that by using two capacitance probe assemblies as described it is possible to measure water level to an accuracy of plus or minus 2 mm in calm conditions.

The measurement of the capacitance of one probe may alternate with the measurement of the capacitance of the other probe, or the measurements may be made simultaneously.

In an especially preferred method of the invention, the level of water in the boiler is monitored by a water level monitoring device capable of monitoring a multiplicity of water levels extending over a range, the water level is monitored at a plurality of different times and the monitoring results at the different times compared to assess whether or not the water is turbulent.

An ability to assess whether or not the water is turbulent enables a further safety factor to be introduced: for example, when other controls indicate that the boiler is producing steam, then the water in the boiler should be turbulent and an assessment of lack of turbulence may be regarded as an indication of a fault. It should be understood that in the context of this specification the term “turbulence” is applied to any disruption to a level water surface, such as may be caused by a wave, by a bubble of steam reaching the surface or by foam on the surface.

Preferably the water level monitoring device is capable of monitoring the water level continuously over its range.

The times of monitoring are preferable separated from one another by less than one half of one second, and more preferably by less than one quarter of one second. In an embodiment of the invention described below the rate of monitoring is ten times per second. The rate is preferably substantially shorter than the period of a wave. Preferably a plurality of monitoring results spanning a time period containing more than one peak of water level are combined together to provide a measure of the water level; that enables a reasonably accurate measurement of water level to be obtained, even when the water is turbulent. Preferably the combining together of the results is weighted in favour of results indicating a relatively low water level; we have found that in turbulent water in a boiler, the peaks of water level contain very little water; thus in an embodiment of the invention described below, the highest and lowest water level results contained in the time period are noted and an inference of the actual level obtained by giving nine times more weight to the lowest level result than to the highest level result.

Preferably the assessment of whether or not the water is turbulent is used as an input to a control unit for controlling the burner.

Preferably a pair of water level monitoring devices are provided. Preferably the water level monitoring devices are capacitance probe assemblies. Preferably, an average of signals from one device is combined with an average of signals from the other device to provide an assessment of the water level.

An especially preferred method of the invention further includes the step of assessing in a control unit the mass flow of steam from the boiler by processing of input signals including ones enabling assessments to be made of:

-   -   a) the heat generated by combustion in the burner     -   b) the temperature and pressure of the steam generated by the         boiler     -   c) the heat dissipated other than in the steam.

It should be understood that a designer is able to make some selections as to how accurate the assessments of a) to c) above are to be and therefore how many variables are to be measured and how accurately they are to be measured. For example, in order to assess the heat dissipated other than in steam an operator might merely measure the temperature of the combustion products and assume a certain further dissipation of heat by other means such as conduction, convection and radiation from the boiler housing.

By making an assessment of the mass flow of steam from measurements of other variables, the need for an expensive steam flow meter is avoided. Although it may appear that the measurement of several other variables in order to assess the steam flow is unnecessarily expensive and complicated, that need not be so because the other variables may be mainly or entirely ones that are being measured anyway for the purpose of controlling the operation of the pressurised steam boiler and burner.

Variables measured to assess the heat generated by combustion in the burner may include the rate of feeding of fuel to the burner, and/or the composition of the combustion products.

Variables measured to assess the heat dissipated other than in the steam may include the temperature of the combustion products and/or the rate of feeding fuel to the burner.

In GB 2169726A, the description of which is incorporated herein by reference, a fuel burner control system is described which includes flue gas sampling and analysing apparatus and which also includes a burner controller which is the subject of GB 2138610A, the description of which is also incorporated herein by reference. That control system already receives inputs relating to the rate of feeding fuel to the burner, the composition of the exhaust gases and the temperature of the exhaust gases. Furthermore it is common for a pressurised steam boiler control system to include sensors for measuring the temperature and pressure of the steam generated by the boiler. Thus it can be seen that all the variables required for the assessment of the mass flow of steam from the boiler may already be available without any extra sensors being required. If desired, however, one or more extra sensors may be provided. For example, a sensor for measuring the temperature of the water being fed into the boiler may be provided.

The assessment of the mass flow of steam from the boiler may be used only as a measure of the flow at a moment in time, or it may also or alternatively be used to provide an assessment of the aggregate amount of steam generated over a certain extended period of time. In the latter case, it may be necessary to allow for other losses within the system, when making the assessment, for example it may be appropriate to assume that a certain percentage of heat is lost during blow down of a boiler. For example an overall loss of 6 percent might be allowed for.

The present invention further provides a method of monitoring the level of water in a pressurised steam boiler, the method including the steps of providing a pair of capacitance probe assemblies mounted in the boiler with each of the probes extending through a range of water levels, the probes being arranged such that the capacitance of each probe varies according to the level of the water, and of measuring the capacitance of each probe, comparing the capacitances to one another to check that they match and using the measurement of the capacitance as an indication of the water level.

The present invention yet further provides a method of assessing in a control unit the mass flow of steam from a pressurised steam boiler by processing input signals including ones enabling assessments to be made of:

-   -   a) the heat generated by combustion in the burner     -   b) the temperature and pressure of the steam generated by the         boiler     -   c) the heat dissipated other than in the steam.

Although the invention has been defined above with reference to a method, it will be understood that it may also be embodied in an apparatus comprising a pressurised steam boiler. Thus the present invention still further provides a pressurised steam boiler including

-   -   a boiler housing for containing water in the boiler,     -   a burner for heating water in the boiler and converting the         water into steam,     -   a water level detector for monitoring the level of water in the         boiler, a pressure detector for detecting the pressure of steam         in the boiler,     -   a firing rate detector for detecting the firing rate of the         burner, and     -   a control unit which receives input signals from the water level         detector, the pressure detector and the firing rate detector and         is operative to control the flow rate of water into the boiler         in dependence upon said input signals.

The present invention still further provides a pressurised steam boiler including:

-   -   a boiler housing for containing water in the boiler, and     -   a water level detector for monitoring the level of water in the         boiler, the water level detector comprising a pair of         capacitance probe assemblies mounted in the boiler housing with         each of the probes extending through a range of water levels,         the probes being arranged such that the capacitance of each         probe varies according to the level of water, and a control and         processing system for measuring the capacitance of each probe,         comparing the capacitances and providing an output signal         indicative of water level based on the capacitance measurements.

The present invention still further provides a pressurised steam boiler including:

-   -   a boiler housing for containing water in the boiler,     -   a burner for heating water in the boiler and converting the         water into steam,     -   a pressure detector for detecting the pressure of steam in the         boiler,     -   a temperature detector for detecting the temperature of steam in         the boiler,     -   a fuel flow detector for measuring the flow rate of fuel into         the burner,     -   a further temperature detector for detecting the temperature of         the exhaust gases,     -   a control unit for receiving and processing input signals from         all of said detectors and for assessing indirectly the mass flow         of steam from the boiler.

The present invention still further provides a pressurised steam boiler including:

-   -   a boiler housing for containing water in the boiler.     -   a water level monitoring device capable of monitoring a         multiplicity of water levels extending over a range, and     -   a control unit for storing results of monitoring the water level         at a plurality of different times and for comparing the results         to assess whether or not the water is turbulent.

It will be appreciated that features described above with respect to methods of controlling the operation of a pressurised steam boiler, methods of monitoring the level of water in a pressurised steam boiler, methods of assessing the mass flow of steam from a pressurised steam boiler and methods of monitoring turbulence in a pressurised steam boiler may be incorporated, wherever that is possible, in any of the pressurised steam boilers as described above. Furthermore, a feature described with respect to one of the methods described above may also be incorporated, wherever that is possible, in any of the other methods described above.

BRIEF DESCRIPTION OF THE SEVERAL VIEWS OF THE DRAWINGS

By way of example, an embodiment of the invention will now be described with reference to the accompanying drawings, of which:

FIG. 1 is a schematic drawing of a burner and a pressurised steam boiler and of a control unit for controlling the burner and steam boiler,

FIG. 2 is a schematic drawing of the pressurised steam boiler of FIG. 1,

FIG. 3 is a sectional view of one of a pair of capacitance probe assemblies employed in the pressurised steam boiler shown in FIG. 2, and

FIG. 4 is a block circuit diagram of the signal control and processing arrangement provided in each capacitance probe assembly.

DETAILED DESCRIPTION OF THE INVENTION

Referring first to FIG. 1, there is shown a burner 20 having a burner head 21, a combustion chamber 22 and a duct 23 for combustion products which comprise exhaust gases. As will be described below the duct 23 passes through a pressurized steam boiler; thereafter the exhaust gases are vented through a flue.

Air is fed to the burner head 21 from an air inlet 24, through a centrifugal fan 26 and then through an outlet damper 27. The burner head 21 is able to operate with either gas or oil as the fuel; gas is fed to the burner head from an inlet 28 via a valve 29 whilst oil is fed to the burner head from an inlet 30 via a valve 31.

A control unit 1 is provided for controlling the operation of the burner and boiler. The control unit 1 has a display 2, a proximity sensor 3 for detecting that a person is nearby, and a set of keys 5 enabling an operator to enter instructions to the control unit. The purpose of the proximity sensor is not relevant to the present invention and will not be described further herein; its purpose is described in GB2335736A, the description of which is incorporated herein by reference.

The control unit 1 is connected to various sensing devices and drive devices, as shown in the drawing. More particularly the unit is connected via an exhaust gas analyser 37 to an exhaust gas analysis probe 38 (which includes a temperature sensor), and to a flame detection unit 40 at the burner head. The control unit 1 is also connected via an inverter interface unit 41 and an inverter 42 to the motor of the fan 26 (with interface unit 41 receiving a feed back signal from a tachometer 26A associated with the fan 26), via an air servo motor 44 to the air outlet damper 27, to an air pressure sensing device 45 provided in the air supply duct downstream of the outlet damper 27, via fuel servo motors 46 to the fuel valves 29, 31 and to a further servo motor 47 for adjusting the configuration of the burner head 21.

The connections described above relate to the control of the burner 20 by the control unit 1. The control unit 1 is, however, also connected, via an RS485 link 48 to a further controller 49, which is shown in FIG. 2 and whose functions are described below.

The combustion chamber 22 of the burner 20 is arranged inside a boiler 50 in a conventional manner. In FIG. 1 the boiler 50 is shown schematically in chain dotted outline. Although FIG. 1 suggests that the combustion chamber leads directly to the exhaust duct 23, it will be understood by those skilled in the art that in practice the gaseous products of combustion follow a serpentine path passing through the boiler 50 a few times before reaching the exhaust duct 23 and being exhausted to atmosphere.

FIG. 2 provides a schematic representation of the boiler and shows a boiler housing 51 which in normal use is filled to approximately the height shown by dotted line LI in FIG. 2. It will be appreciated that the combustion chamber and ducting for the exhaust gases are not shown in FIG. 2.

A water pipe 52 feeds water into the bottom of the boiler at a rate determined by settings of a variable speed pump 53 and via a motorized control valve 54. A temperature detector 59 senses the temperature of the water as it enters the boiler.

A steam outlet pipe 55 takes steam under pressure from the top of the boiler 51. The pressure of the steam taken from the boiler housing 51 is sensed by a pressure detector 56 while its temperature is sensed by a temperature detector 57. Mounted in the top of the boiler housing 51 are a pair of capacitance probe assemblies 58A and 58B. The capacitance probe assemblies are identical to one another and one is described below with reference to FIGS. 3 and 4.

The further controller 49 receives input signals from the following (excluding the connection via the RS485 link 48 to the control unit 1):

-   -   a) each of the capacitance probe assemblies 58A and 58B;     -   b) the steam temperature detector 57;     -   c) the inlet water temperature detector 59;     -   d) the control valve 54 (a feedback signal indicating the degree         of opening of the control valve 54); and     -   e) the pump 53 (a feedback signal indicating the setting of the         pump).

In addition a signal from the pressure detector 56 is passed back along a line 60 (not shown in FIG. 1) to the control unit 1 where it provides an input signal representing demand to the control unit.

The further controller 49 provides output signals to the following (excluding the connection via the RS485 link 48 to the control unit 1):

-   -   i) the control valve 54 (to adjust the degree of opening of the         valve);     -   ii) the pump 53 (to adjust the setting of the pump);     -   iii) a warning light and audible alarm 61A, 61B, respectively,         which are activated when the water level falls to a first low         water level below its normal operating range “first low”);     -   iv) a warning light and audible alarm 62A, 62B, respectively,         which are activated when the water level falls to a second low         water level below the first water level (“second low”); and     -   v) a warning light and audible alarm 63A, 63B, respectively,         which are activated when the water level rises to a high water         level above its normal operating range.

It will be understood that the particular warning light and audible alarms that are employed may be varied from one application to another according to what is required.

In FIG. 2, the dotted line LI indicates the centre of the normal operating range of water level in the boiler. Also shown is a dotted line L2 marking the “first low”, a dotted line L3 marking the “second low” and a dotted line L4 marking the high water level.

Referring now also to FIG. 3, it can be seen that each capacitance probe assembly 58A, 58B includes a main body 70 and an elongate probe 71 which projects downwardly into the interior of the boiler and extends through the high water level (L4), the normal operating level (L1), the “first low” (L2) and the “second low” (L3). Since boilers vary in size the probes 71 are manufactured in various lengths and an appropriate length of probe is chosen for each boiler. For example, the probes may be available in lengths of about 0.5 m, 1.0 m and 1.5 m.

Each probe 71 is formed from a central steel bar 72 surrounded by a sleeve 73 of dielectric material. Also a plug 74 of dielectric material is provided at the free end of the sleeve 73 to seal that end of the probe. Thus, in a manner that is know per se, the probe 71 forms together with the medium surrounding the sleeve 73 a variable capacitance. Since the capacitance is very dependent on whether the medium is water or steam the value of the capacitance is dependent upon how great a length of the probe is surrounded by water rather than steam. Thus, the capacitance of the probe provides an indication of the level of water in the boiler, for all levels between, and including, L3 and L4.

Within the main body 70 of the capacitance probe assembly, there is a secure physical and electrical connection to the probe and a printed circuit board 75 is mounted in an enlarged rear portion 76 of the main body 70, the board 75 carrying the necessary processing circuitry, which is shown in block diagram form in FIG. 4.

Referring now also to FIG. 4, there is shown the probe 71 marked as a varying capacitance, a reference capacitance 77, a relay 78 for alternately connecting the probe 71 and the reference capacitance in the circuit, an oscillator 79, a processor 80 which both controls the operation of the relay 78 and together with the oscillator 79 is able to provide a measure of the capacitance being sensed by detecting the frequency of a signal in a circuit incorporating the capacitance, and a driver 81 which transmits a signal from the probe assembly to the further controller 49. The connection between each probe assembly 58A, 58B and the further controller 49 is made via RS485 links.

In a particular example of the invention, the probe capacitance varies from 10 pF to 200 pF, the reference capacitance 77 is 120 pF, the oscillator 79 is a 555 Type Oscillator, the processor 80 is an 80188 processor and the sleeve 73 is 12 mm outside diameter, 6 mm inside diameter and is made of PTFE (polytetra-fluoroethylene). As the probe capacitance varies due to a change in water level the frequency of the output from the probe assembly alters; typically, the frequency output is of the order of 45,000 Hz and a change of 1 mm in water level alters the frequency by 20 Hz.

When connected in the control system shown in FIGS. 1 and 2, the capacitance of each probe 71 is measured alternately with the reference capacitance 77 of that probe. In the event of a change in temperature, that affects values of both the capacitance of the probe 71 and its reference capacitance 77, so that the change in value of the reference capacitance can be used to adjust the signal from the probe capacitance to compensate for such a temperature change. Also the controller 49 reads signals from each of the probe assemblies 58A, 58B alternately, although, if preferred, simultaneous readings may be obtained. Typically in a steam boiler, the water is somewhat turbulent at least near the surface and that is liable to give rise to some inaccuracy in the measurement made. Thus the controller 49 is arranged to allow for some discrepancy in the signals from the probe assemblies 58A, 58B, but apart from that checks both that the signal of the reference capacitance indicates the correct value of capacitance and that each of the probes 71 indicates the same value of capacitance and therefore the same water level. One particular way in which turbulence in the water can be allowed for and indeed even taken advantage of is described later.

The use of the two identical probe assemblies 58A, 58B each with its own reference capacitance for checking purposes and with all readings from both probe assemblies being checked against one another, results in an especially safe system.

The normal operation of the burner and boiler will be well understood by those skilled in the art from the description above and will not be described further herein. GB2138610A and GB2169726A both provide further details of the normal operation of the burner. The boiler operates in a conventional manner when the water level is normal and, via the controller 49, feeds back signals, for example indicating a dropping steam temperature, to the control unit 1. In the event that the water level in the boiler drops to below the average normal level, then the controller 49 is programmed to adjust the speed of the pump 53 at the water inlet to allow more water into the boiler; similarly, in the event that the water level in the boiler rises gradually a little above the average normal level, then the controller 49 is programmed to close the control valve 54 or reduce the speed of the pump 53 at the water inlet to allow less water into the boiler. In either case, however, the operation of the burner 20 is not affected because the output signals from the control unit 1 are not altered.

If, however, for example, the water level in the boiler falls to the level L2 shown in FIG. 2, then the controller 49 reacts in various ways: firstly the warning light 61A and audible alarm 61B are actuated; secondly a signal is passed back via the RS485 link 48 to the control unit 1 which then shuts down the burner 20 by turning off the supplies of fuel and air to the burner head 21; thirdly, the inlet flow of water into the boiler 5 is increased by adjustment of the control valve 54 and/or the pump 53.

Provided that the water level then rises back towards the level L1, the controller 49 can reverse the measures described in the paragraph immediately above. If for some reason, however, the water level continues to fall, for example because the water inlet is blocked, then when it reaches the level L3 in FIG. 2 the warning light 62A and the audible alarm 62B are activated and a further control signal sent from the controller 49 to the control unit 1, preventing the burner from being turned back on without manual intervention by an operator.

Similarly, if the water level in the boiler rises to the level L4 shown in FIG. 2, then the controller 49 reacts in various ways: firstly the warning light 63A and the audible alarm 63B are activated; secondly a signal is passed back via the RS485 link 48 to the control unit 1 which then shuts down the burner 20 by turning off the supplies of fuel and air to the burner head; thirdly, the inlet flow of water into the boiler 5 is stopped by adjustment of the control valve 54 and/or the pump 53.

The linking of the control of the boiler and the control of the burner enables other more sophisticated and advantageous control techniques to be adopted. In particular, whereas a skilled person would expect the system to be programmed simply so that, whenever the water level rose, the inlet flow rate of water was reduced, that need not be the case.

Although a rise in water level in the boiler is usually a result of the amount of steam leaving the boiler per unit time being less at that time than the amount of water coming into the boiler per unit time, it is possible, paradoxically, for the rise in water level to occur even when the rate at which steam is leaving the boiler is greater than the rate at which water is coming into the boiler. As explained above, that can arise when there is a sudden demand for steam leading to a reduction in pressure in the boiler and consequent expansion of the small bubbles within the water in the boiler, causing the water to expand and thus the water level to rise. The embodiment of the invention described herein is able to identify this special circumstance as will now be described.

The reaction to an increasing water level is determined by assessing within the control system also how the steam pressure in the boiler, which is measured by the detector 56, is changing and how the firing rate of the burner 20, which can for example be assessed from the information in the control unit 1 of the amount of fuel being fed to the burner, is changing. The variables of water level, steam pressure and firing rate can each be sensed at one second intervals and their movements over the last twenty seconds used to assess the cause of an increase in water level.

For example, in a case where the water level is increasing at a slow rate, the pressure in the boiler is increasing at a slow rate and the firing rate is reducing, that is a good indication that the increase in water level is simply caused by a reduction in the demand for steam. Thus, in response to the control unit 1 and the controller 49 receiving signals indicative of that situation, the controller 49 acts to reduce at a slow rate the amount of water per unit time entering the boiler through the pipe 52.

On the other hand, in a case where the water level is increasing at a fast rate, the pressure in the boiler is reducing at a fast rate and the firing rate is increasing, that is a good indication that the increase in water level is actually a result of a sudden demand for steam. Thus, in response to the control unit 1 and the controller 49 receiving signals indicative of that situation, the controller 49 may act to maintain, at its current rate, or to increase the amount of water per unit time entering the boiler through the pipe 52.

It will be appreciated that the precise control criteria that are applied can be varied by the designer of the control system and/or by the commissioning engineer who installs the control system. For example, the system may be arranged so that, if only one probe assembly detects a water level beyond an acceptable range, the alarm and/or burner shut down procedure is commenced only after a relatively long period, for example 20 seconds, whereas, if both probe assemblies detect a water level beyond an acceptable range, the alarm and/or burner shut down procedure is commenced sooner, for example after 10 seconds. As well as selecting values for what may be regarded as a “slow” or “fast” rate of change of a variable, it is also of course possible to introduce values of other variables in the decision-making process for controlling the water level. By combining the control of the burner and the boiler as described above such arrangements become possible.

In a particularly advantageous embodiment, the controller 49 reads a water level signal from each of the probe assemblies 58A, 58B every tenth of a second. To form a water level signal the highest and lowest values are taken from ten consecutive readings from a probe and one tenth of the difference between the values is added to the lowest value to define what is then regarded as the value for that probe. The same procedure is carried out for the other probe and the two values so obtained averaged to provide a good measurement of water level even when the water is turbulent. We have found that taking only one tenth of the difference between the values is appropriate: a characteristic of a typical wave in a boiler is that peaks of the wave are significantly narrower than troughs; for that reason and because of other forms of turbulence, the peaks in the turbulent water contain relatively little water. Thus, in this particular embodiment a water level reading is generated every second; that reading may itself then advantageously be combined with, say, nine other similar readings to provide an average reading that covers a ten second period. That average reading may be updated at any selected rate down to once per second.

The readings from each probe are also used in this particularly advantageous embodiment to detect turbulence. As will now be understood, the probe assemblies 58A, 58B can be expected to give readings with short term variations when there is turbulence; more particularly the readings can be expected to fluctuate considerably over a period of a second when there is turbulence. The control system already described is knowledgeable of the pressure in the boiler and the water temperature and therefore knows whether or not the water should be boiling and therefore turbulent. Changes in water level of 2.5 mm or more in the course of one second may be regarded as indicative of turbulence and thus it is possible to arrange for the control system to conduct a further check that the probe assemblies 58A and 58B are operating properly. In the event of a conflict between the inputs, an alarm may be sounded and/or the burner 20 turned off.

Some degree of tolerance of a difference between the readings from the probe assemblies 58A and 58B is desirable, but it is also desirable that if the readings are far apart and remain far apart for a period long enough to allow for transient variations, then an alarm is sounded and/or the boiler 20 turned off. For example, the system may be arranged to allow for a disparity in water level readings from the respective probe assemblies of up to 50 mm for up to 20 seconds.

The control system described above is also able to assess the amount of steam per unit time that is leaving the boiler and, therefore, can dispose with the need for one or more steam flow meters. The assessment is accomplished by assessing all the energy input per unit time into the burner and boiler and the energy output per unit time other than in the steam. The difference between the energy input and the energy output as so assessed is of course a measure of the energy that has been put into the water/steam in the boiler. Provided the approximate temperature of the water passed into the system is known and the temperature and pressure of the steam are also known it becomes possible to calculate the mass flow rate of the steam. The accuracy with which the energy inputs and outputs are assessed is a matter of design choice, but one particular example is given below.

The energy input to the system is regarded as consisting exclusively of the heat generated from combustion of the fuel in the burner 20. The control unit 1 is able to compute the amount of fuel being combusted and, if desired, can also take into account the exhaust gas analysis results from the analyser 37 to arrive at the rate of energy input at any one time. During commissioning of the control unit 1, a calibrated fuel meter may be used in order that the control unit 1 is able to store a value of the fuel flow rate and/or heat energy input corresponding to each of a plurality of settings of the fuel valve. The control unit 1 is then able to arrive at appropriate values for any intermediate settings by interpolation.

The energy outputs from the system, apart from the steam are regarded as comprising the following:

-   -   i) the energy in the hot exhaust gases after they have passed         through the boiler;     -   ii) losses from the burner and boiler in heat that is         transferred to the surroundings via radiation, conduction and         convection.

The control unit 1 is informed of the temperature of the exhaust gases from the exhaust gas analyser 37 and is able to compute the flow rate of exhaust gases from the amounts of fuel and/or air being fed to the burner. For the losses from the burner and boiler, it is assumed that a fixed percentage of the heat input (in a particular example 0.25%) is lost when the burner is running at maximum firing rate and that the amount of heat lost remains the same at lower firing rates so that if the burner is turned down to, for example, one quarter of its maximum firing rate the percentage loss increases fourfold (in the particular example to 1%).

Thus the control unit 1 is able to assess the energy input into the water in the boiler. From the controller 49 the temperature of the water fed into the boiler is known and the temperature and pressure of the steam leaving the boiler are also known. The heat required to heat water (specific heat) to convert water to steam (latent heat) and to bring steam to a certain temperature and pressure is of course all well established and therefore the data available from the controller 49 when taken with that from the control unit 1 enables the new flow rate of the steam to be computed.

Extra work is required during initial commissioning of the system to calibrate the control unit 1 and the controller 49 so that they provide a good indication of the steam flow rate, but once the commissioning process has been completed and appropriate values stored in look-up tables, the computation of the steam flow rate is automatic.

Thus it can be seen that by linking together the control of the burner and boiler an especially advantageous control system can be provided.

Whilst one particular example of a system has been described, it should be understood that the system may be varied in many respects. For example, in the described embodiment the control unit 1 and the controller 49 are separate physical units; it is, however, possible to locate the controller 49 within the control unit 1 and indeed, if desired, the controller 49 may be integrated wholly into the control unit 1, so that for example they share the same microprocessor. 

1. A method of monitoring turbulence in a pressurised steam boiler, the method including the step of providing a water level monitoring device capable of monitoring a multiplicity of water levels extending over a range, monitoring the water level at a plurality of different times, and comparing the results of monitoring to assess whether or not the water is turbulent in which the times of monitoring are separated from one another by less than one half of one second.
 2. A method according to any of claims 1, in which the assessment of whether or not the water is turbulent is used as an input to a control unit for controlling the operation of a burner that heats the water in the boiler.
 3. A method according to any of claims 1, in which a pair of water level monitoring devices are provided.
 4. A method according to claim 3, in which the water level monitoring devices are capacitance probe assemblies.
 5. A method according to claim 3, in which an average of signals from one device is combined with an average of signals from the other device to provide an assessment of the water level.
 6. A method of monitoring turbulence in a pressurised steam boiler, the method including the step of providing a water level monitoring device capable of monitoring a multiplicity of water levels extending over a range, monitoring the water level at a plurality of different times, a plurality of monitoring results spanning a time period containing more than one peak of water level to provide a measure of the water level, and comparing the results of monitoring to assess whether or not the water is turbulent.
 7. A method according to claim 6, in which the combining together of the results is weighted in favour of results indicating a relatively low water level.
 8. A pressurised steam boiler including: a boiler housing for containing water in the boiler, a burner heating water in the boiler, a water level monitoring device capable or monitoring a multiplicity of water levels extending over a range, and a control unit for storing results of monitoring the water level at a plurality of different times and for comparing the results to assess whether or not the water is turbulent; wherein the control unit assesses whether or not the water is turbulent for controlling the operation of the burner.
 9. A pressurised steam boiler according to claim 8, in which a pair of water level monitoring devices are provided.
 10. A pressurised steam boiler according to claim 9, in which the water level monitoring devices are capacitance probe assemblies.
 11. A pressurised steam boiler according to claim 8, wherein the control unit monitors times separated from one another by less than one half of one second.
 12. A pressurised steam boiler according to claim 8, wherein the plurality of times span a time period containing more than one peak of water level to provide a measure of the water level.
 13. A pressurised steam boiler according to claim 12, the control unit combines the results and weights in favor of results indicating a relatively low water level.
 14. A pressurised steam boiler according to claim 8, wherein a pair of water level monitoring devices are provided.
 15. A pressurised steam boiler according to claim 14, wherein the water level monitoring devices are capacitance probe assemblies.
 16. A pressurised steam boiler according to claim 14, wherein the control unit combines an average of signals from one device with an average of signals from the other device to provide an assessment of the water level. 